Act like a helpful tutor and exlain me : Give step-by-step solution with explanation and final answer:clearly explain all sub partscesgeis FeoosRiy gEEcisd ESESRES © giilEce d3fgesd LER 1 Ii i Hi | Eg gi i ~38 SI i op:
Question:
Act like a helpful tutor and exlain me :
Give step-by-step solution with explanation and final answer:clearly explain all sub partscesgeis
FeoosRiy
gEEcisd
ESESRES
© giilEce
d3fgesd
LER 1
Ii
i Hi
|
Eg
gi i
~38
SI
i op:
This is AI generated Response.
Asked by: manish kumar
Created at: 2025-10-11 08:46:44
Asked by: manish kumar
Created at: 2025-10-11 08:46:44
Final Answer:
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Let's break down and solve the problem **step-by-step**.
---
## **Given Data**
- **Flow rate, \( Q \):** \( .030 \, \text{m}^3/\text{min})
- **Convert to \( \text{m}^3/\text{s} \):**
\[
Q = \frac{.030}{60} = .0005 \, \text{m}^3/\text{s}
\]
- **Velocity at inlet, \( V_1 \):** \( 1.5 \, \text{m/s} \)
- **Diameter at inlet, \( D_1 \):** \( 1.5 \, \text{cm} = .015 \, \text{m} \)
- **Velocity at outlet, \( V_2 \):** \( 5 \, \text{m/s} \)
- **Diameter at outlet, \( D_2 \):** \( .5 \, \text{cm} = .005 \, \text{m} \)
- **Gauge pressure at outlet, \( P_2 \):** \( 15 \, \text{psi} = 103.4 \, \text{kPa} \)
- **Density of water, \( \rho \):** \( 100 \, \text{kg/m}^3 \)
- **Momentum-flux correction factor, \( \beta \):** \( 1.04 \)
---
## **(a) Calculate the inlet area (\( A_1 \))**
\[
A_1 = \frac{\pi}{4} D_1^2 = \frac{\pi}{4} (.015)^2 = \frac{\pi}{4} \times .000225 = .000177 \, \text{m}^2
\]
---
## **(b) Calculate the gauge pressure at the hose inlet (\( P_1 \))**
Use the **Bernoulli Equation** (for horizontal hose, neglecting height difference):
\[
P_1 + \frac{1}{2}\rho V_1^2 = P_2 + \frac{1}{2}\rho V_2^2
\]
Solve for \( P_1 \):
\[
P_1 = P_2 + \frac{1}{2}\rho (V_2^2 - V_1^2)
\]
Plug in values:
- \( P_2 = 103.4 \times 10^3 \, \text{Pa} \)
- \( \rho = 100 \, \text{kg/m}^3 \)
- \( V_2 = 5 \, \text{m/s} \), \( V_1 = 1.5 \, \text{m/s} \)
\[
P_1 = 103400 + \frac{1}{2} \times 100 \times (25 - 2.25)
\]
\[
= 103400 + 500 \times 22.75
\]
\[
= 103400 + 11375
\]
\[
= 114775 \, \text{Pa} = 114.8 \, \text{kPa}
\]
**Final Answer (b):**
\[
\boxed{P_1 = 114.8 \, \text{kPa}}
\]
---
## **(c) Calculate the anchoring force (magnitude and direction)**
### **Step 1: Mass flow rate**
\[
\dot{m} = \rho Q = 100 \times .0005 = .5 \, \text{kg/s}
\]
### **Step 2: Apply the momentum equation (control volume form):**
\[
F_x = \sum (\text{momentum out}) - \sum (\text{momentum in}) + (P_1 A_1 - P_2 A_2)
\]
For a steady flow, horizontal hose:
\[
F_x = \beta_2 \dot{m} V_2 - \beta_1 \dot{m} V_1 + (P_1 A_1 - P_2 A_2)
\]
Given \( \beta_1 = \beta_2 = 1.04 \):
Let's calculate each term:
#### **Momentum terms:**
\[
\dot{m} = .5 \, \text{kg/s}
\]
\[
\beta_2 \dot{m} V_2 = 1.04 \times .5 \times 5 = 2.6
\]
\[
\beta_1 \dot{m} V_1 = 1.04 \times .5 \times 1.5 = .78
\]
#### **Pressure force terms:**
\[
A_1 = .000177 \, \text{m}^2
\]
\[
A_2 = \frac{\pi}{4} (.005)^2 = .0000196 \, \text{m}^2
\]
\[
P_1 A_1 = 114775 \times .000177 \approx 20.3 \, \text{N}
\]
\[
P_2 A_2 = 103400 \times .0000196 \approx 2.03 \, \text{N}
\]
#### **Total anchoring force:**
\[
F_x = (2.6 - .78) + (20.3 - 2.03)
\]
\[
= 1.82 + 18.27
\]
\[
= 20.09 \, \text{N}
\]
**Direction:**
The force acts **opposite** to the flow direction, i.e., to hold the hose in place.
---
## **Final Answers**
### **(a) Area at the inlet**
\[
\boxed{A_1 = .000177 \, \text{m}^2}
\]
### **(b) Gauge pressure at the hose inlet**
\[
\boxed{P_1 = 114.8 \, \text{kPa}}
\]
### **(c) Anchoring force required (magnitude and direction)**
\[
\boxed{20.1 \, \text{N} \text{ (opposite to flow direction)}}
\]
---
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